Water-organic separator tank



March 11, y1958 w. E. BURNS WATER-ORGANIC sEPARAToR TANK 5 Sheets-Sheet 1 Filed sept. 1o. 1953 INVENTOR. W. E. BURNS ATTORNEYS March 1v1, 1958 f w. E. BURNS 2,826,306

WATER-ORGANIC SEPARATOR TANK Filed Sept.` l0. 1953 Sheets-Sheet 2 INVENTOR. W. E. BURNS t t 2 7 K ATTORNEY;

` wQE. BURNS WATER-ORGANIC SEPARATOR TANK yMarch 11, 195s :s sheets-sheet 3 K Filed Seplz.` 10. 1953 AT TORNEYS United States Patent O WATER-ORGANIC. SEPARATGR TANK William Burns, Pasadena, rTex., assigner to Phillips Petroleum Company, a corporation of Delaware ApplicationtSeptember ;.1953, SerialNo. 37.95354)-` 9 Claims. (CIZ 21.0-1'14) This invention relates to the. separation of substantiallyY inthe rate of flow of each of, said liquids through a,

separation zone is. substantially independent of the rate of. ilow of the other of said liquids. In another aspect this invention relates to a, method. for the separation of two substantially immiscible liquids wherein the/volume of each liquid within a separation zone can be. controlled,` In another aspect this invention relates to a method for the separation of two substantially immiscible liquids wherein only a small volume of one of said liquids is maintained within. a separation zone.v In another aspect this invention relates to apparatus for. the separation of two substantially immiscible liquids. In another aspect this invention relates to separator ap.- paratus having adjustable means for varying the volume of each of two substantially immiscible liquids within said separator apparatus. In still another aspect this invention relates to separation means wherein the level of one liquid in a separation zone is varied in accordance with the level of said liquid in a succeeding zone.

In theoperation of chemical plants, oil refineries and other processing` plants, large volumes of water are used for cooling and processing purposes. In some of these operations, particularly ink cooling operations, the water is used on a once through basis. That is, itl is'pumped from a` source of'water such as a natural bay, river, etc., throughheat exchange tubes or jackets in the equipment to be cooled and returned to` said source at a point removed from the intake point. During the circulation of the water through the plant, it'becornesA contaminated with oil, chemicals or other immiscible and/ or insoluble contaminants. If such contaminated water is returned to the source, there is created an: undesirable pollution problem, as well as a loss of more or less valuable oils and/ or chemicals. In other cooling operations the water is pumped from. an artificial' pond,. through the. equipment to be cooled and returned to said'pond; In, such instances the contaminants picked' up by the. water separate therefrom and accumulate in. said pond unless independent separation means are provided.` In other of these operations, particularly in: Some processing operations, tlie water isv frequently injected. directly into the processing operation. at. somepoint as. aquench, Wash, extraction medium,Y etc.. In` such instances. the, injected water generally mustbe-separated tromthe` iinal product. In all.` of these. operations it. is, desirable. for economic reasons to. eiiect the most eicient separation.

Suha separation. as that described becomes dittieult when the volume of onek of the liquids to be separated I2,826,306 Patented Mar. lil, 1958 2. is small compared to the. volume of the other liquid. When one ot the liquids to be separated is: costly, it is desirable to maintains the smallest volumeY possible inV the separation apparatus. Likewise, when, one of theliquids has af tendency to change chemically uponprof longed contact with the other liquid, it is desir-able: to.- reduee the volume, and thereby the residencetime, of such aliquid in the. separating apparatus to a` minimum. Similarly, if one of. they liquids has anv inherent.. tendency toychangechemically, e. g., to polymerize, it is desirable. to. isolate and. maintain a minimumY ofsuch a liquid in the separating apparatus.

Thev prior art' provides various methods and apparatus4 for. the separation. of substantially immiscible liquids. However, none ofA the` prior art provides a method or. apparatus. fiorY separating, substantially immiscible liquids wherein provision is made for isolating the separated liquids in separate compartments, nor where the volume ot either liquid can be maintained at a minimum, and where, once the operation isadjusted the ratioof ilow of the dierent liquids are substantially independent'of each other.

I have discovered that. more efficient separation of` substantially immiscible liquids can be accomplished when the. relative volumes of said liquidssin a separa,y

tion zone` are controlled in accordance with the level of one. of said. liquids in` a succeeding zone.`

According.l to this invention, there is provided ametlifY od of. separating substantially immiscible liquids which: comprises passing` af mixture of= saidliquids into: agravity separation. zone. wherein said liquids: separate to form. an interface, passing saidi separated liquids into separatev succeeding zones, and controlling theflevel of saidinter.- facey in` accordance. with the level ofthe. heavier of said liquids4 in its said. separate zone.

Also according tothis invention, there is provided a separator chamber for separating substantially immisf cible liquidswhich is comprised of a gravityI separation:

compartment the downstream side. ot which: isf defined by a first wein of fixed height, a light liquid: Comparo ment downstream,y from said gravity separation com.-

partment, and. a heavyliquid compartment downstream.-

from saidllight liquid compartment, the downstreannside of said heavy liquid compartment being defmed by a second Weir of a. height less than, but adjustabley relative tothe height of said` rst Weir'.

Figure 1 is. a planA view, partly in section-off` oneform.`

employment of the invention in the manufactured methyl ethyl pyridine and methyl vinyl pyridine.

Figure 5 isan end view, in section, showing.` an adjust able Weir in a cylindrical apparatus.

Referring to the drawings, in` Figures l andV 2, there is illustrated diagrammatieally a separation chamber 11i having` inlet means 10v for'introducing aimixture of sub'- stantially. immiscible liquids into a gravity separationv compartment 12. A plurality of transverse baies 13f secured. toy the bottom `and alternate sides of said compartment, in spaced relationship with each other, extend' partially across said compartmenty so as toprovide a tortuous path for the How of'liquids therethrough. Said bailies can be of any convenient height relative to the overall dimensions of saidchamber.. Spaced apart down-- streamfrom. thelast ofi said battles 13 isa rst Weir 14- aezasoe secured to the bottom and opposite side walls of charnber 11. Said weir 14 which has a height less than that of the last battle 13 serves as the downstream wall of gravity separation compartment 12. Spaced apart downstream from said weir 14 is a partition 15 secured to the bottom and side walls of chamber 11. Partition 15 which has a height preferably greater than that of weir 14 serves as the downstream wall of, and denes, together with the side walls of chamber 11, and the weir 14, light liquid compartment 16. Spaced apart downstream from said partition 15 is a second weir having a top section 17 and a lower section 18. Said lower section 18 is secured to the bottom and side walls of chamber 11. Said top section 17 is movable vertically by means of threaded rod 19 attached thereto and extending through bonnet 20 and is held slidably adjacent to lower section 155 by means of suitable channels 21. Said weir sections 17 and 18 serve as the downstream wall and dene, together with the side walls of chamber 11 and partition 15, a first heavy liquid compartment 22. A second heavy liquid compartment 23 downstream and adjacent to compartment 22 is defined by weir sections 17 and 18, and the walls of chamber 11. Conduit 24 provides for the passage of heavy liquid from compartment 12 to compartment 22.

Light liquid is withdrawn from `compartment 16 through conduit 25 controlled by motor valve 26 actuated by iloat level control 27. Heavy liquid is withdrawn through conduit 28 controlled by motor valve 29 actuated by float level control 30. If desirable or necessary the pressure in chamber 11 can be controlled by pressure relief valve and vent 33. Said pressure relief valve can be set to relieve at a predetermined pressure or can be controlled in accordance with operating conditions of the system in which the separator chamber is employed. Suitable means (not shown) can be provided for draining said chamber when necessary or desirable.

ln operation a mixture of two substantially immiscible liquids having different specific gravities is introduced through conduit 10 into gravity separation compartment 12 of separator vessel 11. Said mixture ows around bales 13 as shown by the arrows in Figure l, during which time a gravity separation occurs and the lighter of the liquids rises and oats on top of the heavy liquid forming interfacial level 31. The separated lighter liquid overflows weir 14 into compartment 16 from which it is withdrawn through conduit 25. The level in compartment 16 is controlled by iloat level controller 27 which Iactuates motor valve 26. The separated heavier liquid flows through conduit 24 into compartment 22 and overows weir section 17 into compartment 23 from which it is withdrawn through conduit 28. The level in cornpartrnent 23 is `controlled by float level controller 30 which actuates motor valve 29.

When liquid is overflowing weir section 17, and liquid is overowing weir 14, the interface 31 is established at a point depending upon (l) the difference between the height of weir 14 and weir section 17 and (2) the speciiic gravity of the two liquids. Since the weight of a column of liquid in compartment 12 must equal the Weight of a column of liquid in compartment 22, these same factors determine the amount of light liquid floating on top of the heavy liquid in compartment 12. In other words, the interface 31 will establish itself at a point below the level 32 by an amount directly proportional to the difference of the specific gravities of the two liquids and dependent upon the difference in height between the two weirs 14 and 17. As the height of weir 17 approaches the height of weir 14 the amount of light liquid iiowing on the heavier liquid in compartment 12 becomes less.

Figure 3 illustrates in diagrammatic form another embodiment of the invention which provides for a greater effective length of weir section 17 relative to the effective length of weir 14. The operation of this embodiment is the same as that described for the embodiment shown in Figures 1 and 2. The relation between the effective lengths of weir 14 and weir section 17 is discussed below.

Figure 4 illustrates in diagrammatic form the employment of the invention in a plant for the manufacture of methyl ethyl pyridine and methyl vinyl pyridine. A mixture of methyl ethyl pyridine and water is removed from fractionation zone 4i) through line 41 into separator 42 wherein a separation between the organic liquid and water is effected as described above. Water is withdrawn from separator 42 through line 43 and recycled as shown. Methyl ethyl pyridine is passed from separator 42 through line 44 to fractionation zone 45 from which a mixture of water and methyl ethyl pyridine is removed overhead through line 46 and returned to separator 42. Dry, purified methyl ethyl pyridine is withdrawn through line 47 to storage tank 48. Methyl ethyl pyridine is dehydrogenated in dehydrogenation zone 49 and the reaction product, methyl vinyl pyridine, is quenched with water at 50. The resulting mixture is passed to separator 51 wherein a separation between the organic liquid and water is eifected as described above. Water is withdrawn from separator 51 through line 52 and recycled as shown. Wet, impure methyl vinyl pyridine is withdrawn from separator 51 through line 53 to fractionation zone 54 from which dry, pure methyl vinyl pyridine is passed through line 55 to storage tank 56. A stream of water and methyl vinyl pyridine is removed overhead from fractionation zone 54 through line 57 and recycled to separator 51. For simplification, only one separator 51 is shown as serving both dehydrogenation zone 49 and fractionation zone 54. In actual practice, if desired, an individual separator can be employed for each zone. Separators 42 and 51 were constructed in accordance with the invention.

Figure 5 is an end view showing a Weir that can be used in the invention when using a cylindrical apparatus. This weir can be adjusted for height in a horizontal cylindrical Vessel. The operation of this weir is similar to that described under Figure 2. Section 58 is movable vertically by means of threaded rod 19A attached thereto and extending through bonnet 20A and is held slidably adjacent to lower section 18A by means of suitable channels 57.

Example I A substantially cylindrical vessel approximately seven feet in diameter, constructed in accordance with the invention, was employed for the separation of a mixture of methyl ethyl pyridine and water. It was found that a completely satisfactory separation between the two liquids could be eifected. The layer or organic chemical oating on top of the water in the gravity separation compartment was approximately 6 inches thick. The height of the water overflow Weir was 66.0 inches and the height of the pyridine overflow weir was 66.38 inches. The specific gravity of the organic chemical phase was 0.90 and the specific gravity of the water phase was 0.96.

Example I! A substantially cylindrical vessel approximately l0 feet in diameter, constructed in accordance with the invention, was employed to effect a completely satisfactory separation of a mixture of methyl vinyl pyridine and Water. The layer or organic chemical floating on top of the water in the gravity separation compartment was approximately 3 inches thick. The height of the water overow weir was 90.0 inches and the height of the pyridine overilow weir was 90.12 inches. The specic gravity of the organic chemical phase was 0.92 and the specific gravity of the water phase was 0.96.

From the heights of the weirs in both the above examples, it can be seen that the pyridine layer was maintained in the smaller upper portion of the separation Chamber, thus, further reducing the inventory of the expensive organic chemical Iin Ithe apparatus.

"In theV E above ltexa'rnples it vwas tdesirable f to "maintain the `minimumf-"volumef "the LAligliterli'quid -in the separator. vvThe invention 'can- Ialso Abe vtilize'dflwhenit is1 desirable Ato Vmaintain V4a=-`irrinirnumvolume ofC theheavier of two -irnmiscibleliquidsl lin fthe' separator. f Infisuchy instances l the f conduit JvI4 which extends dthrough i Weir 14 and partitionIS (Figure 2)`-is placed-iat orf'near-f'theflbottom `r`f t-lleAW chamber L'and'fthe *height "of weir Ysection .17 is" niadef'rrl'chless'l than that fweir`-'1`4.

@For 'example, 'the #invention 'can be 'employed llas a catalyst separator in those processes which employ a heavy liquid catalysti sufchfas"A hydr'uoric acid :or aluminum? chlorideeh'ydrocarbon complex,

Examplelll Howeverpvessels ofother shapes can be employed. One

particularly vusefulifembodiment ofi the 'invention comprises a substantially cylindrical vessel having the'isarne arrangement of 5 compartments, baliies, -partitions, rweirs, etc.,r asl thatl `describedffor `the *e'm'bddimntillustrated` in Figures l andZ. `As illustrated* in FExample` Il above; the embodiment employing f' a substantially f cylindrical vessel is= especially valuable in -thoseinstances where'in'one of the `'liquids/tolbe separated has aften'dency to -poly-mer'ize upon standing. ."As `mentior'iedi@above,.rbyliproper-adjustment'fofrtneseveralwein heightstoztakeadvantage of the vessel shape, :'the lvolume -oflthe llnolymerizalaleliquid` within the separatorcan bemaintainedrfat anfabsolute minimum. Y

It is within'thelscope vof.^the'inver1'tionlfor'-thelseparation chamber to :comprisea rectangularlgravity -separaration -Icompartment `fand fcylindrical -light land 'hea'vy liquid compartments 'or vice versa. Y It is`I alsovwithin' the scope Vof 'the' invention for 'the' several compartments-to be non-'adjacent and @connected to-teachi other 'by T suitable conduits.

In Figuresl land 2,-the adjustable weir-was'fillust-rated as being rectangular-in shape; ofy two'sectionsiandextend-y ingientirelyfacrossthefchanben l Obviously, it -Wouldf ibe within the scope of the invention to employ weirs-fdifferent shapes and different effective lengths. For example, the said Weir. could comprise4 a partitionwith a center section of adjustable height or two side sections of adjustable height servingasthe electiveblength of the Weir.

Also, -it .isfwithin "the scope .of the kinvention toprovide forboth of vthedescr'ibe'd weirs to befadjustablewin` height relative--to each other. In such` instances at least ane adjustment Tin effective Weir heights-can -be made-at the upstream weir (weir'14 inFigure 2).

As mentioned above, the invention provides a method and apparatus for the separation of substantially immiscible liquids which, once adjusted, will operate substantially independently of the several liquid flow rates. After determining the height of Weir 17 in relationship to the height of Weir 14, Weir 17 can be fixed in place. The invention has been described assuming normal liuctuations of the several liquid flow rates. However, in those instances where unusually large fluctuations in the flow rate of the heavier liquid are encountered, the embodiment of the invention illustrated in Figure 3 is preferable.

As the flow of liquid over a weir increases, the head over the-we`i increases there'ifective'heighteo theeweir. Therefore, `an abnormal increase 1in 't-he `volurnefoftheavy liquid' passingvr through `the -apparatus off IFigure V2f would result in an increase in the effective -heig'ht yo'f'weirlsection I7. This could resultin raising the interface 31 `toa point 'where there'fwould be danger.ofheavyfliquid spilling over Weir-14 intoV lightliquid compartmentl 16. I'Ihis danger'can bem'itigated `byincreasing'the effective length of '-weir sectioni 17 f relative-to that4 of -l-weirl 14 fasfshown in l Figure'S. Y An increaseffin fhead Loverthekweir resulting in an increase inthcfetective'heightffofweir section 17 wo'uld-'stillresultin;lacorrespondngriseof the interface 31. However, the-1greater1eflective llength fof Weir section-17 r'willi accommodate -all 'butf' the most'` abnormalincrases in heavy fliquidlflow.

The embodiment illustrated `inFigurc f21 `lisfespe'cially valuable when separating liquids off extremely close :specific gravity. lnsuch instances the-'location tof` 4the inter- Vface in theegravity-separation compartment'changes radically-with any change -inlthe eie'ctive height'of the heavy liquid 4over-ilow Weir (Weir 1section17).

Reasonable variation1 and modification are 4'possible within the `-scope of I theabove specification,y the idrawings,- and the appended claims-tto the invention, the essence of which lis a -methodand apparatus for the separation of substantially immiscible fliquids which-comprises lseparation of-said liquids inV a: gravity separation zone 4to forman` interface therein, passingI said separated liquids into separate zones, and Acontrolling the level of said interface lin accordance with the level of the `heavier of said liquids in itsf'saidlseparatezone.

lli claim:

. l. Apparatus for= the `separation vof -substantiallyl' irnmiscible liquids which comprises a separation vessel having: a lgravityr separation compartment-deiinedfby the wallsof said vessell and\a'rst*-weir of liixedehei'ght-ex tending transversely across said vessel; a'plurality'of transverse'bailies lextending'alternatelyfrom opposite side walls andpartiallyfacrosssaid compartmena light liquid compartment :downstream from andeadjacent'to `said gravity-separation compartment -andfdefiined 'by saidirst Weir, thewalls ofsaid vessel-and afpartition :extending transverselyncross said l vessel; a iirst: I`heavy liquid` compartmentl'downstream from said gravity'- separation compartment-andadjacent'to saidlight liquid compartmentfan'd defnedliby" said partition;v `theivvalls of said* vesselland la second weir,w said lsecond Weir havinga--heightl less 'than butvariablerelative to the'height of said 4irstweir; a second heavy lliquid kcompartment downstream from and adjacent to* saidi -rst heavy -liquid 'compartment andY defined bysaid-fsecondweir andltherwalls 'of said vesselya conduit-connecting saidv gravity separation compartment andA saidfrst hea'vy liquid-compartment; and means for varyingtheheight offsaidlse'cond Weir.

2 Apparatus for the separation of substantiallyimmiscible -liquids'lwhich comprises -a substantially cylindrical vessel 'having a'pair of end w'alls anda cylindrical wall; `a first upstream compartment dened byrone of said endwa'lls,` said cylindrical wall,"and a `tirstweirse cure-d to said cylindrical Awall and extending rtransversely across :said fvessel; Iaspluralityt 5f-transversel baiiles in spaced relationship with each other in said first compartment secured to said cylindrical wall and extending alternately from opposite sides thereof partially across said compartment so as to provide a tortuous ow of liquid therethrough; saidv irst Weir having a fixed height less than that of said transverse baiiie in closest proximity thereto; a second compartment downstream from and adjacent to said first compartment and dened by said rst Weir, said cylindrical wall and a transverse partition extending `across said vessel and secured to said cylindrical wall; a conduit extending through said first Weir and said partition; a third compartment downstream from said rst compartment and adjacent to said second compartment and defined by said partition, said cylindrical wall and a second Weir having a height less than but variable relative to the height of said first weir; means for varying the height of said second weir; a fourth compartment downstream from and adjacent to said third compartment and defined by said second Weir, said cylindrical wall, and the other of said end walls; inlet means into said first compartment; outlet means from said sec ond compartment controlled by level control means responsive to a liquid level therein; and outlet means from said fourth compartment controlled by level control means responsive to a liquid level therein.

3. Apparatus for the separation of substantially immiscihle liquids which comprises a separation vessel having: a gravity separation compartment defined by the walls of said vessel and a first weir of fixed height extending transversely across said vessel; a light liquid compartment downstream from and adjacent to said gravity separation compartment and defined by said first weir,

the walls of said vessel and a partition extending transversely across said vessel; a first heavy liquid compartment downstream from said gravity separation compartment and adjacent to said light liquid compartment and defined by said partition, the walls of said vessel and a second weir, said second weir having a height less than,

but variable relative to the height of said first weir; a 7

second heavy liquid compartment downstream from and adjacent to said first heavy liquid compartment and defined by said second weir and the walls of said vessel; a conduit connecting said gravity separation compartment and said first heavy liquid compartment; and means for varying the height of said second weir.

4. An apparatus according to claim 3 wherein the effective length of said second Weir is greater than that of said first weir.

5. An apparatus according to claim 3 wherein the effective length of said second weir is less than that of said first weit.

6. Apparatus for continuously separating substantially immiscible light and heavy liquids which is comprised of, in combination: a gravity separation compartment the downstream side of which is defined by a first Weir of fixed height extending transversely across said compartment; -a light liquid compartment positioned downstream from and adapted to receive light liquid from said gravity separation compartment; a heavy liquid compartment positioned downstream from and adapted to receive heavy liquid from said gravity separation compartment, the downstream sidc of said heavy liquid compartment being defined by a second weir having a height less than, but variable relative to the height of said first weir and exending transversely across said heavy liquid compartment; and means without said heavy liquid compartment and 'attached to said second weir for Varying the height of said second Weir during continuous operation of said apparatus.

7. Apparatus for the separation of substantially immiscible liquids which comprises a separation vessel having: a gravity separation compartment defined by the walls of said vessel and a first Weir extending transversely across said vessel; a light liquid compartment downstream from and adjacent to said gravity separation compartment and defined by said first Weir, the walls of said vessel and a partition extending transversely across said vessel; a first heavy liquid compartment downstream from said gravity separation compartment and adjacent to said light liquid compartment and defined by said partition, the walls of said vessel and a second weir, said second Weir having a height less than but variable relative to the height of said first Weir; a conduit connecting said gravity separation compartment and said first heavy liquid compartment; and means for varying the height of said second weir.

8. Apparatus for continuously separating substantially immiscible light and heavy liquids which is comprised of, in combination: a gravity separation compartment the downstream side of which is defined by a first weir of fixed height extending transversely across said compartment; a light liquid compartment positioned downstream from and adapted to receive light liquid from said gravity separation compartment; a heavy liquid compartment positioned downstream from and adapted to receive heavy liquid from said gravity separation compartment; a second .veir of variable height defining the downstream side of and extending transversely across said heavy liquid compartment, said second weir having a lower section and a vertically movable upper section mounted slidably adjacent said lower section; and means without said heavy liquid compartment and attached to said upper section for slidably raising and lowering said upper section of said second Weir during continuous operation of said apparatus.

9. Apparatus for continuously separating substantially immiscible light and heavy liquids which is comprised of, in combination: a gravity separation compartment the downstream side of which is dened by a first Weir of fixed height extending transversely across said compartment; a light liquid compartment positioned downstream from and adapted to receive light liquid from said gravity separation compartment; a heavy liquid compartment positioned downstream from and adapted to receive heavy liquid from said gravity separation cornpartment; a second weir of variable height defining the downstream side of and extending transversely across said heavy liquid compartment, said second weir having a lower section and a vertically movable upper section mounted slidably adjacent said lower section; a rod threaded at one end and attached to said upper section at the other end, said threaded end extending without said heavy liquid compartment through a threaded bonnet; and means for turning said rod in said bonnet so as to slidably raise and lower said upper section of said second weir during continuous operation of said apparatus.

References Cited in the file of this patent UNTTED STATES PATENTS 368,544 Morrison Aug. 16, 1887 1,170,558 Nonnenbruch Feb. 8, 1916 1,513,882 Bateman Nov. 4, 1924 1,873,597 Jones Aug. 23, 1932 2,083,861 Padgett June 15, 1937 

1. APPARATUS FOR THE SEPARATION OF SUBSTANTIALLY IMMISCIBLE LIQUIDS WHICH COMPRISES A SEPARATION VESSEL HAVING: A GRAVITY SEPARATION COMPARTMENT DEFINED BY THE WALLS OF SAID VESSEL AND A FIRST WEIR OF FIXED HEIGHT EXTENDING TRANSVERSELY ACROSS SAID VESSEL, A PLURALITY OF TRANSVERSE BAFFLES EXTENDING ALTERNATELY FROM OPPOSITE SIDE WALLS AND PARTIALLY ACROSS SAID COMPARTMENT; A LIGHT LIQUID COMPARTMENT DOWNSTREAM FROM AND ADJACENT TO SAID GRAVITY SEPARATION COMPARTMNET AND DEFINED BY SAID FIRST WEIR, THE WALLS OF SAID VESSEL AND A PARTITION EXTENDING TRANSVERSELY ACROSS SAID VESSEL; A FIRST HEAVY LIQUID COMPARTMENT DOWNSTREAM FROM SAID GRAVITY SEPARATION COMPARTMENT AND ADJACENT TO SAID LIGHT LIQUID COMPARTMENT AND DEFINED BY SAID PARTITION, THE WALLS OF SAID VESSEL AND A SECOND WEIR, SAID SECOND WEIR HAVING A HEIGHT LESS THAN BUT VARIABLE RELATIVE TO THE HEIGHT OF SAID FIRST WEIR; A SECOND HEAVY LIQUID COMPARTMENT DOWNSTREAM FROM AND ADJACENT TO SAID FIRST HEAVY LIQUID COMPARTMENT AND DEFINED BY SECOND WEIR AND THE WALLS OF SAID VESSEL; A CONDUIT CONNECTING SAID GRAVITY SEPARATION COMPARTMENT AND SAID FIRST HEAVY LIQUID COMPARTMENT; AND MEANS FOR VARYINF THE HEIGHT OF SAID SECOND WEIR. 